TUNING A PH PID
CONTROLLER
Julia Fletcher
Renee Chuang
Anthony Yeoman
Jiayue Yu
University of California, San Diego
Jacobs School of Engineering
A batch system, with a strong acid and
base was under investigation.
Transmits Signal
(http://ucsd-ceng-176.wikia.com)
The PBS solution was titrated to identify
the buffer region.
0
2
4
6
8
10
12
0 50 100 150 200
pH
Time(s)
Titration Curve
Buffer Region = 6.5 - 7.8 pH
An open loop step change was used to
determine Kp & 𝜏 of the system.
KKp: .000954
𝜏: 24.17
The Direct synthesis method was used to
derive equations for controller coefficients.
System
Model
Controller Coefficients
The coefficients found via direct synthesis was
observed to reach set point at 120 seconds.
7.2
7.3
7.4
7.5
7.6
7.7
7.8
7.9
8
8.1
0 20 40 60 80 100 120 140 160
pH
Time(s)
𝐾𝑐 = 6.074
𝜏 𝐷= 24.17
Controller coefficients were doubled and
compared to each other.
7.2
7.4
7.6
7.8
8
8.2
8.4
0 20 40 60 80 100 120 140
pH
Time(s)
Double Kc
Double tau_deri
Direct Synthesis
Set point
In summary, direct synthesis is a favorable tuning
method when trying to control pH.
(www.setis-systems.com)
In summary, direct synthesis is a favorable tuning
method when trying to control pH.
Questions?(www.setis-systems.com)

Tuning a pH PID Controller

  • 1.
    TUNING A PHPID CONTROLLER Julia Fletcher Renee Chuang Anthony Yeoman Jiayue Yu University of California, San Diego Jacobs School of Engineering
  • 2.
    A batch system,with a strong acid and base was under investigation. Transmits Signal (http://ucsd-ceng-176.wikia.com)
  • 3.
    The PBS solutionwas titrated to identify the buffer region. 0 2 4 6 8 10 12 0 50 100 150 200 pH Time(s) Titration Curve Buffer Region = 6.5 - 7.8 pH
  • 4.
    An open loopstep change was used to determine Kp & 𝜏 of the system. KKp: .000954 𝜏: 24.17
  • 5.
    The Direct synthesismethod was used to derive equations for controller coefficients. System Model Controller Coefficients
  • 6.
    The coefficients foundvia direct synthesis was observed to reach set point at 120 seconds. 7.2 7.3 7.4 7.5 7.6 7.7 7.8 7.9 8 8.1 0 20 40 60 80 100 120 140 160 pH Time(s) 𝐾𝑐 = 6.074 𝜏 𝐷= 24.17
  • 7.
    Controller coefficients weredoubled and compared to each other. 7.2 7.4 7.6 7.8 8 8.2 8.4 0 20 40 60 80 100 120 140 pH Time(s) Double Kc Double tau_deri Direct Synthesis Set point
  • 8.
    In summary, directsynthesis is a favorable tuning method when trying to control pH. (www.setis-systems.com)
  • 9.
    In summary, directsynthesis is a favorable tuning method when trying to control pH. Questions?(www.setis-systems.com)

Editor's Notes

  • #3 Flow chart of experimental procedure
  • #6 Gc, transfer model Equation for tau and kc Start at low end then progress to high end of buffer region(insert #s)
  • #9 Advise for future groups Difficulties Not enough time to test out other tunning methods and although we did receive good results we don't have any results to compare it by to see if this is the best tuning method.
  • #10 Advise for future groups Difficulties Not enough time to test out other tunning methods and although we did receive good results we don't have any results to compare it by to see if this is the best tuning method.